JPH08277341A - Production of microporous sheet - Google Patents

Production of microporous sheet

Info

Publication number
JPH08277341A
JPH08277341A JP10467595A JP10467595A JPH08277341A JP H08277341 A JPH08277341 A JP H08277341A JP 10467595 A JP10467595 A JP 10467595A JP 10467595 A JP10467595 A JP 10467595A JP H08277341 A JPH08277341 A JP H08277341A
Authority
JP
Japan
Prior art keywords
microporous sheet
resin
dispersion
average particle
substrate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP10467595A
Other languages
Japanese (ja)
Inventor
Hiroshi Hasegawa
博史 長谷川
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sanyo Chemical Industries Ltd
Original Assignee
Sanyo Chemical Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sanyo Chemical Industries Ltd filed Critical Sanyo Chemical Industries Ltd
Priority to JP10467595A priority Critical patent/JPH08277341A/en
Publication of JPH08277341A publication Critical patent/JPH08277341A/en
Pending legal-status Critical Current

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  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)

Abstract

PURPOSE: To simply produce a microporous sheet, good in mechanical properties without containing an organic solvent and causing any danger of toxicity and useful as a natural leather substitute by dispersing a powder of an organic polymer in an aqueous resin, applying the resultant dispersion to a substrate and then drying the applied dispersion. CONSTITUTION: (A) A powder of an organic polymer (e.g. nylon) is dispersed in (B) an aqueous resin (preferably a polyurethane resin emulsion) at 100:(3-300) solid weight ratio of the components (A):(B) and the resultant dispersion is applied to a substrate and then dried. In detail, the component (A) having 5-500μm average particle diameter is dispersed in the component (B) and the prepared dispersion is applied to the substrate and dried. A dispersion prepared by dispersing the component (A) having 0.1-50μm average particle diameter in the component (B) is further preferably applied thereto and dried.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は微多孔性シートの製造方
法に関する。さらに詳しくは、機械的性質、透湿性等の
諸性能に優れた微多孔性シートを高い生産性で製造する
方法に関するものである。得られた微多孔性シートは、
天然皮革代替品、繊維コーティング製品等として利用さ
れる。
FIELD OF THE INVENTION The present invention relates to a method for producing a microporous sheet. More specifically, the present invention relates to a method for producing a microporous sheet excellent in various properties such as mechanical properties and moisture permeability with high productivity. The resulting microporous sheet,
It is used as a natural leather substitute and fiber coating product.

【0002】[0002]

【従来の技術】従来、微多孔性シートの製造方法として
は、ポリウレタン等の有機高分子を水溶性有機溶剤の
溶液として繊維素材に付与し、湿式凝固する方法、乾
式法(例えば特公昭51ー41063号公報および特開
昭51ー41063号公報に記載の方法)、ポリウレ
タン微粒子を含有するポリウレタン樹脂のW/O型エマ
ルションを用いる方法(例えば特開昭62ー27322
0号公報に記載の方法)など知られている。
2. Description of the Related Art Conventionally, as a method for producing a microporous sheet, an organic polymer such as polyurethane is applied to a fiber material as a solution of a water-soluble organic solvent and wet-coagulated, or a dry method (for example, JP-B-51- No. 41063 and JP-A No. 51-41063), and a method using a W / O type emulsion of polyurethane resin containing polyurethane fine particles (for example, JP-A No. 62-27322).
The method described in Japanese Patent No. 0) is known.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上記
の湿式法では、使用される有機溶剤が引火性が強くかつ
毒性が強いため、火災の危険性や溶剤の回収コストが高
い等の問題;の乾式法では、多量の親水性樹脂を使用
するため得られるシート材料の機械的性質が充分とはい
えず、かつその製造方法は煩雑であるとともに乾燥方法
に厳密な温度管理が必要であり、しかも長時間を要する
ので非常に生産性が低い等の問題;のポリウレタン微
粒子を含有するポリウレタン樹脂のW/O型エマルショ
ンを用いる方法では、の場合と同様、使用される有機
溶剤の引火性および毒性等の問題があった。
However, in the above wet method, since the organic solvent used is highly flammable and highly toxic, there are problems such as fire risk and high solvent recovery cost; In the method, since a large amount of hydrophilic resin is used, the mechanical properties of the obtained sheet material cannot be said to be sufficient, and the manufacturing method thereof is complicated, and the drying method requires strict temperature control, In the method using a W / O type emulsion of a polyurethane resin containing polyurethane fine particles, the productivity is very low because it takes time; There was a problem.

【0004】[0004]

【課題を解決するための手段】本発明者らは、上記問題
点を解決する方法について鋭意検討した結果、有機溶剤
を使用する必要がなく、かつ生産性良く微多孔性シート
を製造できる方法を見いだし、本発明に到達した。すな
わち本発明は、有機高分子の粉体(A)を水性樹脂
(B)に、固形分重量比100:(3〜300)で分散
させ、これを基材に付着せしめた後、乾燥することを特
徴とする微多孔性シートの製造方法。
Means for Solving the Problems As a result of intensive investigations by the present inventors on a method for solving the above-mentioned problems, a method for producing a microporous sheet which does not require the use of an organic solvent and which can be produced with high productivity has been found. Found and arrived at the present invention. That is, according to the present invention, the organic polymer powder (A) is dispersed in the aqueous resin (B) at a solid content weight ratio of 100: (3 to 300), and this is adhered to a substrate and then dried. A method for producing a microporous sheet, comprising:

【0005】本発明における有機高分子の粉体(A)と
しては、例えばポリエチレン、ポリプロピレン、ポリブ
タジエン、ポリスチレン、ナイロン、ポリウレタン、ポ
リアミド、ポリアクリル樹脂、ポリエステル、ポリ酢酸
ビニル樹脂、エチレン/酢酸ビニル共重合体、ポリ塩化
ビニル樹脂、エポキシ樹脂等の水に不溶性の樹脂の粉体
が挙げられる。これらの樹脂うち好ましいものは、ナイ
ロン、ポリウレタン、ポリアクリル樹脂、ポリ酢酸ビニ
ル樹脂およびポリ塩化ビニル樹脂である。該(A)の平
均粒径は、通常0.1〜500μmである。平均粒径が
0.1μm未満では微多孔性シートが形成されず、50
0μmを越えると得られる微多孔性シートの機械的強度
が低下する。
Examples of the organic polymer powder (A) in the present invention include polyethylene, polypropylene, polybutadiene, polystyrene, nylon, polyurethane, polyamide, polyacrylic resin, polyester, polyvinyl acetate resin, ethylene / vinyl acetate copolymer. Examples thereof include powders of water-insoluble resins such as coalesce, polyvinyl chloride resin, and epoxy resin. Among these resins, preferred are nylon, polyurethane, polyacrylic resin, polyvinyl acetate resin and polyvinyl chloride resin. The average particle size of the (A) is usually 0.1 to 500 μm. If the average particle size is less than 0.1 μm, a microporous sheet will not be formed, and
When it exceeds 0 μm, the mechanical strength of the obtained microporous sheet is lowered.

【0006】水性樹脂(B)としては、例えばポリウレ
タン樹脂、ウレア樹脂、ポリアクリル樹脂、ポリスチレ
ン樹脂、ポリエステル樹脂、ポリアミド樹脂、ポリイミ
ド樹脂、ポリアミノ酸樹脂、ポリ酢酸ビニル部分ケン化
物、エチレン/酢酸ビニル樹脂、ポリ塩化ビニル樹脂お
よびエポキシ樹脂の水溶液もしくは水性分散体;SB
R、NBR、EPR、ポリブタジエンゴム、ブチルゴ
ム、天然ゴム等のゴムラテックス等が挙げられる。これ
らのうち好ましいものはポリウレタン樹脂、ポリアクリ
ル樹脂、ポリアミド樹脂およびポリ酢酸ビニル部分ケン
化物の水溶液もしくは水性分散体、ならびに、SBRお
よび天然ゴムのラテックスであり、特に好ましいものは
ポリウレタン樹脂の水性分散体である。
Examples of the aqueous resin (B) include polyurethane resin, urea resin, polyacrylic resin, polystyrene resin, polyester resin, polyamide resin, polyimide resin, polyamino acid resin, partially saponified polyvinyl acetate, ethylene / vinyl acetate resin. , Aqueous solution or dispersion of polyvinyl chloride resin and epoxy resin; SB
Examples thereof include rubber latexes such as R, NBR, EPR, polybutadiene rubber, butyl rubber and natural rubber. Among these, preferred are aqueous solutions or aqueous dispersions of polyurethane resins, polyacrylic resins, polyamide resins and partially saponified polyvinyl acetate, and latexes of SBR and natural rubber, and particularly preferred are aqueous dispersions of polyurethane resins. Is.

【0007】(A)と(B)の固形分重量比は、通常1
00:(3〜300)、好ましくは100:(10〜1
00)である。(B)の比率が3未満では、(B)によ
るバインダー効果が乏しくなり、得られるシートの機械
的強度が低下し、300を越えると、得られるシートの
透湿性が低下する。
The solid content weight ratio of (A) and (B) is usually 1
00: (3 to 300), preferably 100: (10 to 1)
00). If the ratio of (B) is less than 3, the binder effect due to (B) will be poor, and the mechanical strength of the obtained sheet will decrease, and if it exceeds 300, the moisture permeability of the obtained sheet will decrease.

【0008】本発明において、(A)と(B)との配合
物を基材に付着せしめるに際し、必要に応じて、メタノ
ール、エタノール等の水溶性溶剤、アルキルフェノール
のアルキレンオキシド付加物等の界面活性剤、カルボキ
シメチルセルロース等の増粘剤、シリコン系化合物等の
消泡剤、フッ素系化合物等のレベリング剤、ポリエポキ
シ化合物、アミノ樹脂等の架橋剤、顔料、マイグレーシ
ョン防止剤等が適宜配合される。
In the present invention, when the mixture of (A) and (B) is attached to the substrate, a surface-active agent such as a water-soluble solvent such as methanol or ethanol, an alkylene oxide adduct of alkylphenol, etc. may be used, if necessary. Agents, thickeners such as carboxymethyl cellulose, antifoaming agents such as silicon compounds, leveling agents such as fluorine compounds, polyepoxy compounds, cross-linking agents such as amino resins, pigments, migration inhibitors, and the like.

【0009】微多孔性シートの基材としては、例えば天
然繊維、半合成繊維、合成繊維などの編布、織布または
不織布や、離型紙、プラスチックフィルム、金属板、ガ
ラス板などが用いられる。
As the base material of the microporous sheet, for example, knitted cloth, woven cloth or non-woven cloth of natural fiber, semi-synthetic fiber, synthetic fiber, release paper, plastic film, metal plate, glass plate and the like are used.

【0010】基材に付着せしめる方法としては、(A)
と(B)とからなる配合物を基材に含浸、コーティン
グ、スプレーなどの方法で処理後、必要に応じて過剰分
を搾液した後、加熱乾燥する方法が挙げられる。乾燥条
件は、基材、付与する分散液組成、付着量等により異な
るが、通常、60〜180℃にて10秒〜10分程度で
ある。乾燥温度が(A)の熱軟化点以上となると、粉体
の融着を生じ、得られる微多孔性シートの柔軟性や透湿
度を低下させるため、熱軟化点の10℃以上低い温度で
実施する。また、基材に付着させる該配合液の量は、そ
の目的に応じて任意に選択されるが、基材1m2当り通
常5〜3000gである。
As a method of adhering to the substrate, (A)
Examples include a method in which a base material is treated with a composition comprising (B) and (B) by a method such as impregnation, coating, or spraying, and then excess liquid is squeezed if necessary, followed by heating and drying. The drying conditions vary depending on the substrate, the composition of the dispersion liquid to be applied, the amount of adhesion, etc., but are usually about 10 seconds to 10 minutes at 60 to 180 ° C. When the drying temperature is equal to or higher than the thermal softening point of (A), fusion of the powder occurs, and the flexibility and moisture permeability of the resulting microporous sheet are reduced. To do. The amount of the compounded liquid adhered to the base material is arbitrarily selected depending on the purpose, but is usually 5 to 3000 g per 1 m 2 of the base material.

【0011】付着せしめる方法において、(A)と
(B)とからなる配合物を一度付着せしめて乾燥後、こ
の上にさらに平均粒径の異なる(A)と(B)の配合物
を付着せしめて乾燥し、多層構造のシートとすることも
可能である。たとえば、平均粒径が5〜500μの
(A)を(B)に分散させ、これを基材に付着せしめて
乾燥後、この上にさらに平均粒径が0.1〜50μの
(A)を(B)に分散させたものを付着せしめて乾燥す
ることにより、得られる微多孔性シートが天然皮革独得
の反発弾性を有し、かつ折り曲げ時に皺が形成されるな
ど高度に天然皮革と類似の物性を発現する。
In the method of adhering, the composition comprising (A) and (B) is once adhered and dried, and then the composition of (A) and (B) having different average particle diameters is further adhered thereon. It is also possible to dry it to obtain a multilayered sheet. For example, (A) having an average particle size of 5 to 500 μ is dispersed in (B), and this is adhered to a substrate and dried, and then (A) having an average particle size of 0.1 to 50 μ is further added. By depositing the dispersion in (B) and drying it, the resulting microporous sheet has unique repulsion resilience of natural leather and is highly similar to natural leather in that wrinkles are formed during folding. Express physical properties.

【0012】[0012]

【実施例】以下実施例により本発明を更に説明するが、
本発明はこれに限定されるものではない。実施例中の部
は重量部、%は重量%を示す。なお、実施例中に用いら
れる各測定値の測定方法は下記の通りである。 透湿度:JIS Z 0208B(g/m2・24h) 柔軟性:ハンドリングによる触感
The present invention will be further described with reference to the following examples.
The present invention is not limited to this. Parts in the examples are parts by weight, and% is% by weight. In addition, the measuring method of each measured value used in an Example is as follows. Water vapor transmission rate: JIS Z 0208B (g / m 2 · 24h) Flexibility: Tactile sensation by handling

【0013】実施例1 ナイロン樹脂の粉体(平均粒径:50μ、熱軟化点:1
50℃)100部、ポリウレタン樹脂エマルション[三
洋化成工業(株)製「パーマリンUA−150」、固形
分濃度:30%)100部および水240部を混合分散
させ、これにカルボキシメチルセルロース3部を加え
て、固形分濃度30%、粘度5000cPの水性分散液
を得た。これをポリエステル(PET)極細繊維不織布
上に、厚さ1mmとなるようコーティングし、100℃
にて10分乾燥して微多孔性シートを得た。
Example 1 Nylon resin powder (average particle size: 50 μ, thermal softening point: 1
50 parts), 100 parts of polyurethane resin emulsion [Sanyo Kasei Kogyo Co., Ltd. "Permarin UA-150", solid content concentration: 30%) 100 parts and 240 parts of water are mixed and dispersed, and 3 parts of carboxymethyl cellulose is added thereto. Thus, an aqueous dispersion having a solid content concentration of 30% and a viscosity of 5000 cP was obtained. This is coated on a polyester (PET) ultrafine fiber nonwoven fabric to a thickness of 1 mm, and the temperature is 100 ° C.
And dried for 10 minutes to obtain a microporous sheet.

【0014】実施例2 ポリウレタン樹脂の粉体(平均粒径:100μ、熱軟化
点:140℃)100部、ポリウレタン樹脂エマルショ
ン[三洋化成工業(株)製「パーマリンUA−15
0」、固形分濃度:30%)100部および水240部
を混合分散させ、これにカルボキシメチルセルロース3
部を加えて、固形分濃度30%、粘度5000cPの水
性分散液を得た。これをPET極細繊維不織布上に、厚
さ1mmとなるようコーティングし、100℃にて10
分乾燥して微多孔性シートを得た。
Example 2 100 parts of polyurethane resin powder (average particle size: 100 μ, thermal softening point: 140 ° C.), polyurethane resin emulsion [“Permarin UA-15” manufactured by Sanyo Kasei Co., Ltd.]
0 ", solid content concentration: 30%) 100 parts and water 240 parts are mixed and dispersed, and carboxymethyl cellulose 3
Parts were added to obtain an aqueous dispersion having a solid content concentration of 30% and a viscosity of 5000 cP. This is coated on a PET ultrafine fiber non-woven fabric to a thickness of 1 mm, and the temperature is 10
Minute drying was performed to obtain a microporous sheet.

【0015】実施例3 実施例2で得た水性分散液を、PET極細繊維不織布上
に、厚さ0.6mmとなるようコーティングし、100
℃にて10分乾燥した後、その上にさらに、アクリル樹
脂の粉末(平均粒径:1μ、熱軟化点:170℃)10
0部、SBRラテックス[日本合成ゴム(株)製「JS
R−0548」、固形分濃度:50%)40部および水
210部を混合分散させ、これにカルボキシメチルセル
ロース2部を加えて、固形分濃度35%、粘度7000
cPとした水性分散液を、厚さ0.4mmとなるようコ
ーティングし、100℃にて10分乾燥して2層構造の
微多孔性シートを得た。
Example 3 A PET ultrafine fiber non-woven fabric was coated with the aqueous dispersion obtained in Example 2 so as to have a thickness of 0.6 mm.
After drying for 10 minutes at ℃, further 10 powder of acrylic resin (average particle size: 1μ, thermal softening point: 170 ℃) 10
0 parts, SBR latex [JS manufactured by Japan Synthetic Rubber Co., Ltd.
R-0548 ", solid content concentration: 50%) 40 parts and water 210 parts are mixed and dispersed, and 2 parts of carboxymethyl cellulose is added thereto to give a solid content concentration of 35% and a viscosity of 7,000.
The cP aqueous dispersion was coated to a thickness of 0.4 mm and dried at 100 ° C. for 10 minutes to obtain a microporous sheet having a two-layer structure.

【0016】実施例4 実施例1で得た水性分散液を、離型紙上に厚さ0.5m
mとなるようコーティングし、100℃にて10分乾燥
して微多孔性シートを得た。なお、透湿度の測定は、離
型紙を剥して試験を行った。
Example 4 The aqueous dispersion obtained in Example 1 was coated on a release paper with a thickness of 0.5 m.
m to obtain a microporous sheet by coating and drying at 100 ° C. for 10 minutes. The moisture permeability was measured by peeling off the release paper.

【0017】比較例1 ポリウレタン樹脂の粉体(平均粒径:100μ、熱軟化
点:140℃)10部、ポリウレタン樹脂エマルション
[三洋化成工業(株)製「パーマリンUA−150」、
固形分濃度:30%)300部および水28部を混合分
散させ、これにカルボキシメチルセルロース2部を加え
て、固形分濃度30%、粘度5000cPの水性分散液
を得た。これをPET極細繊維不織布上に、厚さ1mm
となるようコーティングし、100℃にて10分乾燥し
て比較シートを得た。
Comparative Example 1 10 parts of polyurethane resin powder (average particle size: 100 μ, thermal softening point: 140 ° C.), polyurethane resin emulsion [“Permarin UA-150” manufactured by Sanyo Kasei Co., Ltd.,
300 parts of solid content concentration: 30%) and 28 parts of water were mixed and dispersed, and 2 parts of carboxymethyl cellulose was added thereto to obtain an aqueous dispersion having a solid content concentration of 30% and a viscosity of 5000 cP. Put this on PET ultra-fine fiber non-woven fabric, thickness 1mm
And was dried at 100 ° C. for 10 minutes to obtain a comparative sheet.

【0018】比較例2 ナイロン樹脂の粉体(平均粒径:50μ、熱軟化点:1
50℃)100部、ポリウレタン樹脂エマルション[三
洋化成工業(株)製「パーマリンUA−150」、固形
分濃度:30%)5部および水240部を混合分散さ
せ、これにカルボキシメチルセルロース3部を加えて、
固形分濃度30%、粘度6000cPの水性分散液を得
た。これをPET極細繊維不織布上に、厚さ1mmとな
るようコーティングし、100℃にて10分乾燥した
が、粉体がばらばらで密着せず、シート状物は得られな
かった。
Comparative Example 2 Nylon resin powder (average particle size: 50 μ, thermal softening point: 1
50 parts), 100 parts of polyurethane resin emulsion [Sanyo Chemical Co., Ltd. "Permarin UA-150", solid content concentration: 30%) 5 parts and 240 parts of water are mixed and dispersed, to which 3 parts of carboxymethyl cellulose is added. hand,
An aqueous dispersion having a solid content concentration of 30% and a viscosity of 6000 cP was obtained. This was coated on a PET ultrafine fiber nonwoven fabric so as to have a thickness of 1 mm and dried at 100 ° C. for 10 minutes, but the powder was scattered and did not adhere, and a sheet-like material was not obtained.

【0019】性能試験 実施例1〜4および比較例1で得られたシート状物の性
能評価結果を表1に示す。
Performance Test Table 1 shows the performance evaluation results of the sheet-like materials obtained in Examples 1 to 4 and Comparative Example 1.

【0020】[0020]

【表1】 注)記号の説明 ○:良好,×:不良[Table 1] Note) Explanation of symbols ○: Good, ×: Poor

【0021】[0021]

【発明の効果】本発明の微多孔性シートの製造方法は、
従来技術では達し得なかった下記の効果を有する。 (1)有機溶剤を含有しないので引火や毒性の危険はな
く、かつ溶剤回収設備も必要ないのでコスト的にも有利
である。 (2)親水性樹脂をしないので、得られるシート材料の
機械的性質が良好なシートが得られる。 (3)製造方法が簡便であるとともに乾燥に厳格な温度
管理が必要でなく、しかも短時間で乾燥できるので高い
生産性を確保できる。 (4)構成する樹脂粉体およびバインダー樹脂を広範囲
に選択できるので、幅広い物性の微多孔性シートを製造
できる。 本発明の方法を用いて得られる微多孔性シートは、天然
皮革代替品、繊維コーティング製品等として幅広く利用
できる。
The method for producing a microporous sheet of the present invention comprises:
It has the following effects that cannot be achieved by the conventional technology. (1) Since it does not contain an organic solvent, there is no danger of ignition or toxicity, and no solvent recovery equipment is required, which is advantageous in terms of cost. (2) Since no hydrophilic resin is used, a sheet having good mechanical properties can be obtained. (3) The manufacturing method is simple, and strict temperature control is not required for drying, and moreover, it can be dried in a short time, so that high productivity can be secured. (4) Since the resin powder and the binder resin to be constituted can be selected in a wide range, a microporous sheet having a wide range of physical properties can be manufactured. The microporous sheet obtained by using the method of the present invention can be widely used as a natural leather substitute, a fiber coating product, or the like.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】有機高分子の粉体(A)を水性樹脂(B)
に、固形分重量比100:(3〜300)で分散させ、
これを基材に付着せしめた後、乾燥することを特徴とす
る微多孔性シートの製造方法。
1. An organic polymer powder (A) is replaced with an aqueous resin (B).
In a solid content weight ratio of 100: (3 to 300),
A method for producing a microporous sheet, which comprises depositing this on a substrate and then drying.
【請求項2】平均粒径が5〜500μの(A)を(B)
に分散させ、これを基材に付着せしめて乾燥後、この上
にさらに平均粒径が0.1〜50μの(A)を(B)に
分散させたものを付着せしめて、乾燥することを特徴と
する請求項1または2に記載の微多孔性シートの製造方
法。
2. An (A) having an average particle diameter of 5 to 500 .mu.
And then depositing it on a substrate and drying it, and then depositing (A) having an average particle size of 0.1 to 50 μ dispersed in (B) thereon and drying. The method for producing a microporous sheet according to claim 1 or 2, which is characterized.
【請求項3】(B)がポリウレタン樹脂エマルションで
ある請求項1〜3のいずれかに記載の微多孔性シートの
製造方法。
3. The method for producing a microporous sheet according to claim 1, wherein (B) is a polyurethane resin emulsion.
JP10467595A 1995-04-04 1995-04-04 Production of microporous sheet Pending JPH08277341A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10467595A JPH08277341A (en) 1995-04-04 1995-04-04 Production of microporous sheet

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10467595A JPH08277341A (en) 1995-04-04 1995-04-04 Production of microporous sheet

Publications (1)

Publication Number Publication Date
JPH08277341A true JPH08277341A (en) 1996-10-22

Family

ID=14387054

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10467595A Pending JPH08277341A (en) 1995-04-04 1995-04-04 Production of microporous sheet

Country Status (1)

Country Link
JP (1) JPH08277341A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003048939A (en) * 2001-08-08 2003-02-21 Achilles Corp Method for producing porous polyurethane body
US6765590B1 (en) 1999-08-31 2004-07-20 Matsushita Electric Industrial Co., Ltd. AV device control apparatus
WO2012026368A1 (en) * 2010-08-23 2012-03-01 日東電工株式会社 W/o emulsion, foam, and functional foam
WO2012029537A1 (en) * 2010-08-31 2012-03-08 日東電工株式会社 Foam, production method for foam, and functional foam
JP2012051985A (en) * 2010-08-31 2012-03-15 Nitto Denko Corp Foam excellent in toughness and thermal resistance
JP2012082257A (en) * 2010-10-07 2012-04-26 Nitto Denko Corp Heat-resistant shock-absorbing foam
JP2012082259A (en) * 2010-10-07 2012-04-26 Nitto Denko Corp Heat-resistant low heat-conductive foam

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6765590B1 (en) 1999-08-31 2004-07-20 Matsushita Electric Industrial Co., Ltd. AV device control apparatus
JP2003048939A (en) * 2001-08-08 2003-02-21 Achilles Corp Method for producing porous polyurethane body
WO2012026368A1 (en) * 2010-08-23 2012-03-01 日東電工株式会社 W/o emulsion, foam, and functional foam
WO2012029537A1 (en) * 2010-08-31 2012-03-08 日東電工株式会社 Foam, production method for foam, and functional foam
JP2012051985A (en) * 2010-08-31 2012-03-15 Nitto Denko Corp Foam excellent in toughness and thermal resistance
JP2012082257A (en) * 2010-10-07 2012-04-26 Nitto Denko Corp Heat-resistant shock-absorbing foam
JP2012082259A (en) * 2010-10-07 2012-04-26 Nitto Denko Corp Heat-resistant low heat-conductive foam

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